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US3450393A - Gas and liquid contact apparatus - Google Patents

Gas and liquid contact apparatus
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US3450393A
US3450393AUS468064AUS3450393DAUS3450393AUS 3450393 AUS3450393 AUS 3450393AUS 468064 AUS468064 AUS 468064AUS 3450393D AUS3450393D AUS 3450393DAUS 3450393 AUS3450393 AUS 3450393A
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water
sheets
contact
gas
strips
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US468064A
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Carl Georg Munters
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J1me 1969 c. G. MUNTERS GAS AND LIQUID CONTACT APPARATUS Sheet Filed June 29, 1965 INVENTOR. rj 70); {43's 20 can G June 17, 1969. c. c. MUNTERS 3,450,393
I GAS AND LIQUID CONTACT APPARATUS Filed June 29, 1965sheet 3 of 4 INVENTOR. a Geo r WW; Zgrs GAS AND LIQUID CONTACT APPARATUS Filed June 29. 1965 Sheet of 4 A'VENTOR. Cal/ rief? unl grg June 1969 c. G. MUNTERS GAS AND LIQUID CONTACT APPARATUS Sheet Filed June 29. 1965 oo 5m M v l l 4 a a A 4'//,
v 1 ACA INVENTOR. Carl Q4207 United States Patent 0.
3,450,393 GAS AND LIQUID CONTACT APPARATUS Carl Georg Muuters, 3 Danderydsvagen, Stocksund, Sweden Filed June 29, 1965, Ser. No. 468,064 Claims priority, application Sweden, July 7, 1964, 8,48'2/64 Int. Cl.F24f 3/14 US. Cl. 261-112 2 Claims ABSTRACT OF THE DISCLOSURE This invention relates to a contact apparatus which is provided with a contact body mounted in a housing and which defines a plurality of channels or ducts through which gas and liquid are passed, the liquid being supplied from above by a spreader. This invention finds particular application to a cooling tower in which water is cooled by means of air. The contact body may be of known construction such as a maze of slats and the like although it is preferably provided with corrugations, which form the ducts or channels extending through the packing. In one particularly advantageous embodiment, the corrugations cross each other in adjacent layers forming ducts which continuously vary in width in horizontal, as well as in vertical direction.
One main object of the invention is to produce a spray ing device, which will assure an extremely even diffusion of the liquid despite the fact that it has no movable parts and is simple in construction. According to one main feature of the invention the sprayer comprises one of several slices or the like, which include corrugated sheets embossing one another in adjacent layers, so that vertically extending and sideways directed ducts will be formed for spreading the liquid. In order to impart to the cooling tower the maximum capacity per unit of volume, it is necessary that all the surfaces of the contact body shall be uniformly supplied with water, which according to another feature of the invention is accomplished, even though the water jets, which are arranged above the slice-like sprayer, are spaced relatively large distance from one another.
Further objects and advantages of the invention will become apparent from the following description, considered in connection with the accompanying drawings, which form part of this specification and of which:
FIG. 1 is a vertical longitudinal section of a cooling tower according to the invention;
FIG. 2 is a partial prospective view of the cooling tower packing and the spraying device drawn to an enlarged scale;
FIG. 3 is a vertical longitudinal section of a cooling tower according to a modification;
FIG. 4 is a partial prospective view of the cooling tower packing and spraying device of the modification shown in FIG. 3 drawn to an enlarged scale;
FIG. 5 is a prospective view of a portion of a cooling tower packing and a spraying device according to another modification;
FIG. 6 shows a preferred embodiment of the packing.
Throughout the figures the same reference numerals indicate the same or similar parts.
3,450,393 Patented June 17, 1969 In the embodiment shown in FIGS. 1 and 2 the cooling tower is provided with contact members orpackings 10 which are enclosed within acover 12 and are passed by both media, namely water and air, in cross or countercurrent direction. The contact members ofpackings 10 are composed of thin sheets which preferably are undulated or corrugated and positioned vertically. Thecorrugations 14, 16 in twoadjacent sheets 18, 20 cross one another to form horizontal as well as vertical channels extending through the contact member. Furthermore, these channels vary continuously in width from 0 where the sheets contact one another to a width which is substantially twice the height of the corrugations. The height of the corrugations may range from 5 to 15 mm. or more. The sheets may consist of paper or of plastic materials as disclosed in the copending patent applications Serial Nos. 380,357 and 441,961, filed July 6, 1964, and March 23, 1965, respectively.
The air is admitted to the contact members through theopenings 22 in the cover and pass through the channels in horizontal direction as indicated by thearrows 24, 26. The cover has an outlet opening 28 for the air at the top and in which afan 30 is mounted which is driven by amotor 32.
The water is supplied to the cooling tower through the pipes '34, which along their bottom side are provided withoutlet openings 36 and which are spaced from one another in the longitudinal direction of the pipes. Beneath theopenings 36 are arranged vanes orbafiles 38 upon which the water jets impinge and are broken up.
On top of thecontact members 10 according to the invention, slices orpads 40 are arranged which in the examples shown have the same general construction as the contact members, i.e., may consist of thin sheets 42, 44 which are corrugated or undulating with the corrugations crossing one another. The sheets are positioned in a vertical plane which preferably is perpendicular to the main direction ofsheets 18, 20 of the contact members. The general direction of the latter coincides with the longitudinal direction of thepipes 34. The sheets or foils 42, 44 are preferably composed of a plastic material preferably of the type which does not burn such as polyvinyl chloride. The slice orpad 40 differs from thecon tact members 10* in that the height of the corrugations are substantially smaller than in the latter.
The cooling tower is provided at the bottom with awater sump 46 from which the cooled water is conducted to the place of use through aconduit 48 in which is arranged avalve 50. The water level in thesump 46 is regulated by means of afloat 52 so that additional water may be admitted to replace the water evaporated in the contact members. From the place of use the water is returned to the cooling tower through theconduits 34 to be cooled again. From thepipes 34 the water will run down onto thepad 40. This will cause the water to spread out due to the slanting corrugations so that even the spaces between theconduits 34 will be supplied with a satisfactory amount of water. From thepad 40 the water runs down onto the sheets of the contact members in uniform distribution over the entire frontal area, which in turn has a very advantageous effect on the cooling capacity of the contact member.
The channels in thepad 40 may be so narrow that a bridging may take place at the lower part of the channels due to surface tension or capillary force. However, in this case, it makes no diiference as the air does not pass through the channels of thepad 40. The Water drops down from the bottom openings of the channels in thepad 40 since the vertical height of the pad is greater than the capillary rise in the channels.
A vertical extension of thepad 40 is determined by the desired sideways distribution, which in turn depends upon the mutual spacing between the jet openings or the spacing between the rows of such openings. Another factor is the degree of slope in the corrugations with respect to the vertcial plane, which in turn affects the sideways distribution. This must be at least half the distance between two rows of jet openings, i.e. in the present case the distance between twoconduits 34. According to the invention the water may be supplied through relatively large holes and spaced correspondingly large mutual distances while maintaining an even distribution over the frontal area of the contact member. The risk of the openings being plugged by deposit of scale formations will be lessened by making the openings larger.
In the modifications shown in FIGS. 3 and 4, the two media are passed through thecontact element 10 in counter-current direction. Thus the air is admitted from beneath through theopenings 54 in thehousing 12 and is drawn upwardly through the contact member which extends across the entire cross-sectional area of the housing. The water as in the first embodiment is supplied through theconduits 34 and thespreader slice 40. In view of the fact that the air stream passes upwardly through the pad, it is important that the duct terminals not become bridged entirely or partially by water droplets in such a manner that it will increase the pressure drop of the air in any substantial degree. The effect of the capillary force can to some extent be eliminated by providing good contact between the sheets of the pad with the sheets of thecontact element 10. The risk of plugging will thereby be reduced due to the fact that the water will be passed to the sheets of thecontact element 10 and then further downwardly. The height of the corrugations in thepad 40 in this modification may be somewhat larger than in the previous one in order to reduce the tendency toward bridging of water at the lower surface of the pad.
In this modification the contact element or packing 10 is supported onthin ribs 56, which serve as conductors for the water and thereby counteract the plug formation at the undersurface of the contact element. In this case the distance between theribs 56 is greater than the spacing between the sheets in thecontact element 10. The ribs preferably extend perpendicularly to the plane of thesheets 18, 20.
In order to expedite the passing of the air through thepad 40, the latter may be subdivided into smaller units or strips 58 (FIG. which are spaced from one another at such a distance that the air resistance problem will be eliminated which might cause bridging by water droplets in the sprayer slices 58 or by the air resistance produced by theslice 40 in FIGS. 3 and 4 even with bridging. Between theunits 58 spacing members may be arranged, for instance in the form ofrectangular pipes 60. Thus, in this case the main portion of the air will pass the one side of the sheets or partitions which distribute the water. The jet openings in theconduit 34 are preferably arranged directly above thestrips 58.
In modification shown in FIG. 6 thesheets 18 of the packing member are longer than thesheets 20 so that the former with theirlower edge portions 62 project below the lower edges of thesheets 20. In this manner are provided drainingtips 64 which are wider in width than the average spacing between thesheets 18, 20. Thus, the downwardly flowing water is prevented from bridging the distance between the lower edges of the sheets.
A contact member or packing ordinarily has a vertical height which is many times greater than that of thespreader pad 40 or thestrips 58. In this latter embodiment the contact body is passed by the air as in the embodiment shown in FIGS. 3 and 4. These embodiments may also serve to cool the water and may then have a greater vertical depth.
The packing or contact element may be constructed as disclosed in the U.S. patent specification No. 2,809,818.
While one more or less specific embodiment of the invention has been described, it is to be understood that this is for illustration only, and that the invention is not to be limited thereby, but its scope is to be determined by the appended claims.
What I claim is:
1. A gas and liquid contact device through which liquid flows by gravity in thermodynamic relationship with currents of air being passed therethrough comprising:
(a) at least two superposed units;
(b) each of said units comprising a plurality of facially opposed strips disposed in substantially vertical relationship to form a plurality of intersecting and intercommunicating open-ended passages for allowing passage of gas and liquid therethrough;
(c) the strips in at least the upper one of said units being corrugated with the corrugations in alternate strips crossing the corrugations in the strips disposed between the alternate strips;
(d) the strips in one of said units extending crosswise to the strips of the other unit;
(e) means for supplying liquid to the upper one of said units;
(f) means for passing currents of gas through said passages in contact with the liquid flowing by gravity therethrough; and
(g) the strips in the upper unit being spaced a smaller distance apart than the strips in the underlying unit.
2. A gas and liquid contact device through which liquid flows by gravity in thermodynamic relationship with currents of air being passed therethrough comprising:
(a) at least two superposed units;
(b) each of said units comprising a plurality of facially opposed strips disposed in substantially vertical relationship to form a plurality of intersecting and intercommunicating open-end passages for allowing passage of gas and liquid therethrough;
(c) the strips in at least the upper one of said units being corrugated with the corrugations in alternate strips crossing the corrugations in the strips disposed between the alternate strips;
(d) the strips in one of said units extending crosswise to the strips of the other unit;
(e) means for supplying liquid to the upper one of said units;
(f) means for passing currents of gas through said passages of at least the lower unit in contact with the liquid flowing by gravity therethrough; and
(g) the heightof the upper unit being substantially less than the underlying unit.
References Cited UNITED STATES PATENTS 2,490,080 12/1949 Melvill. 2,783,982 3/1957 Kahl. 3,084,918 4/1963 Kohl et a1. 3,262,682 7/ 1966 Bredberg. 3,243,170 3/1966 Ellis et al. 261-94 FOREIGN PATENTS 571,510 8/ 1945 Great Britain.
TIM R. MILES, Primary Examiner.
US468064A1964-07-101965-06-29Gas and liquid contact apparatusExpired - LifetimeUS3450393A (en)

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Cited By (39)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US3738626A (en)*1970-03-261973-06-12Munters Ab CarlDevice in contact bodies for liquid and gas
US4107241A (en)*1976-10-121978-08-15Raschig G.M.B.H.Contacting arrangement for mass transfer operations
US4233029A (en)*1978-10-251980-11-11Eastman Kodak CompanyLiquid transport device and method
US4290980A (en)*1976-06-121981-09-22Politechnika Slaska Im. Wincentego PstrowdkiegoMass exchanger with packaging
US4294663A (en)*1980-06-181981-10-13Munters CorporationMethod for operating a coke quench tower scrubber system
US4302313A (en)*1979-07-231981-11-24Eastman Kodak CompanyElectrode-containing device with capillary transport between electrodes
US4303600A (en)*1981-01-081981-12-01The Munters CorporationReactor column
US4323536A (en)*1980-02-061982-04-06Eastman Kodak CompanyMulti-analyte test device
US4385012A (en)*1980-01-281983-05-24Ronald PriestleyPhase-contacting apparatus
US4385011A (en)*1980-04-141983-05-24Munters CorporationSloped film fill assembly
FR2518713A1 (en)*1981-12-211983-06-24Moreau ChristianEvaporative air freshener for vehicle - has housing with moistened surface formed by zigzag absorbent air permeable cloths
US4405533A (en)*1977-09-221983-09-20Ab Carl MuntersSupply device for use with evaporative contact bodies
WO1985000021A1 (en)*1983-06-161985-01-03Board Of Control Of Michigan Technological UniversColumn froth flotation
US4499031A (en)*1982-09-271985-02-12Allis-Chalmers Corp.Evaporative gas treating system
US4544513A (en)*1983-04-151985-10-01Arvin Industries, Inc.Combination direct and indirect evaporative media
US4592834A (en)*1983-06-161986-06-03Board Of Control Of Michigan Technological UniversityColumn froth flotation
US4599174A (en)*1984-02-271986-07-08Polybac CorporationSubmerged fixed film biological treatment system
US4678615A (en)*1986-07-231987-07-07Dspie "D. Blagoev"Cooling stack for cooling towers
US4842778A (en)*1985-12-231989-06-27Glitsch, Inc.Apparatus for flow distribution in packed towers
US4934663A (en)*1989-09-201990-06-19Phelps Peter MCooling tower with sloping high density film fill sandwiched between low density film fill
US4950430A (en)*1986-12-011990-08-21Glitsch, Inc.Structured tower packing
US5192464A (en)*1992-04-231993-03-09Lech PawlowskiEvaporative cooler
US5312464A (en)*1993-05-251994-05-17Munters CorporationCross-flow film fill media with drift eliminator
US5762668A (en)*1996-07-241998-06-09Glitsch, Inc.Apparatus and method for deentrainment in a chemical process tower
WO2000011426A1 (en)*1998-08-252000-03-02Agam Energy Systems Ltd.Evaporative media unit for cooling tower
JP3273611B2 (en)1992-01-212002-04-08アルファーラヴァル サーマル アーベー Plate heat exchanger
WO2003004937A1 (en)*2001-07-032003-01-16Agam Energy Systems Ltd.An air conditioning system
US20030086846A1 (en)*2001-11-052003-05-08Adusei George Y.Monolith stacking configuration for improved flooding
RU2262455C1 (en)*2004-06-302005-10-20Московский автомобильно-дорожный институт (Государственный технический университет)Air cleaner
US20060292349A1 (en)*2005-05-052006-12-28Seeley Frederic FAn evaporative material system and method of manufacture
US20070145611A1 (en)*2005-12-232007-06-28Lee Adam TGas-liquid contactor baffle
US20080116592A1 (en)*2005-01-112008-05-22Ff Seeley Nominees Pty LtdMethod and Materials for Improving Evaporative Heat Exchangers
US20080150171A1 (en)*2006-12-222008-06-26Amt International, Inc.Gas-liquid contact apparatus
US20080179766A1 (en)*2007-01-302008-07-31Lee Adam TGas-liquid contact apparatus
US20090189301A1 (en)*2008-01-242009-07-30Amt International, Inc.Downcomer distributor
WO2010089315A3 (en)*2009-02-042013-04-25Universität KasselSystem for dehumidifying, heating and/cooling of a liquid
US9109839B2 (en)2013-06-112015-08-18Akeel Ali WannasMulti-layered evaporative media module for heat exchange apparatus
DE102018120217A1 (en)*2018-08-202020-02-20Tristan Wilms Device and method for the simultaneous biological purification of waste water, in particular waste water with a biodegradable load, and provision of cooled air
USD1071114S1 (en)*2023-03-242025-04-15Yu-Sung LiHeat dissipation mesh

Families Citing this family (5)

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Publication numberPriority datePublication dateAssigneeTitle
US3969447A (en)*1973-10-181976-07-13Fritz W. Glitsch & Sons, Inc.Grids for fluid contact apparatus
DE2937368C2 (en)*1979-09-151982-12-16Buckau-Walther AG, 4048 Grevenbroich Contact body ventilation system
AT380335B (en)*1980-03-251986-05-12Faigle Kunststoff Gmbh FILLED BODY FOR PLANTS FOR ENERGY AND / OR FUEL EXCHANGE OR DROP SEPARATOR AND THE LIKE
DE3021740A1 (en)*1980-06-101981-12-17Vsesojuznyj gosudarstvennyj i proektnyj institut teploelektroproekt, MoskvaSpray cooling for power station - has grid housing, and water distributor with staggered pipes and nozzles
US6478290B2 (en)*1999-12-092002-11-12Praxair Technology, Inc.Packing for mass transfer column

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GB571510A (en)*1943-11-181945-08-28Frederick Gilbert MitchellImprovements in or relating to cooling towers
US2490080A (en)*1944-05-191949-12-06Francis L MelvillContacting apparatus
US2783982A (en)*1955-01-271957-03-05Kahl Carl H WilliamEvaporative cooler with tower air flow
US3084918A (en)*1960-04-211963-04-09Fluor CorpCorrugated packing for counterflow cooling towers
US3243170A (en)*1961-04-201966-03-29Hydronyl LtdTower packing units
US3262682A (en)*1962-06-271966-07-26Munters & Co CarlContact bodies for liquid and gas

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GB249420A (en)*1925-05-281926-03-25Otto SorgeImprovements relating to liquid-cooling towers
FR1138128A (en)*1954-12-211957-06-11 Improvements to heat exchanger devices, particularly water chillers
DE1115750B (en)*1960-01-071961-10-26Otto Stange Trickle cooler
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GB571510A (en)*1943-11-181945-08-28Frederick Gilbert MitchellImprovements in or relating to cooling towers
US2490080A (en)*1944-05-191949-12-06Francis L MelvillContacting apparatus
US2783982A (en)*1955-01-271957-03-05Kahl Carl H WilliamEvaporative cooler with tower air flow
US3084918A (en)*1960-04-211963-04-09Fluor CorpCorrugated packing for counterflow cooling towers
US3243170A (en)*1961-04-201966-03-29Hydronyl LtdTower packing units
US3262682A (en)*1962-06-271966-07-26Munters & Co CarlContact bodies for liquid and gas

Cited By (51)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US3738626A (en)*1970-03-261973-06-12Munters Ab CarlDevice in contact bodies for liquid and gas
US4290980A (en)*1976-06-121981-09-22Politechnika Slaska Im. Wincentego PstrowdkiegoMass exchanger with packaging
US4107241A (en)*1976-10-121978-08-15Raschig G.M.B.H.Contacting arrangement for mass transfer operations
US4405533A (en)*1977-09-221983-09-20Ab Carl MuntersSupply device for use with evaporative contact bodies
US4233029A (en)*1978-10-251980-11-11Eastman Kodak CompanyLiquid transport device and method
US4302313A (en)*1979-07-231981-11-24Eastman Kodak CompanyElectrode-containing device with capillary transport between electrodes
US4385012A (en)*1980-01-281983-05-24Ronald PriestleyPhase-contacting apparatus
US4323536A (en)*1980-02-061982-04-06Eastman Kodak CompanyMulti-analyte test device
US4385011A (en)*1980-04-141983-05-24Munters CorporationSloped film fill assembly
US4294663A (en)*1980-06-181981-10-13Munters CorporationMethod for operating a coke quench tower scrubber system
FR2485029A1 (en)*1980-06-181981-12-24Munters Corp PROCESS FOR EXTINGUISHING COKE AND PURIFYING RESULTING GASES
US4303600A (en)*1981-01-081981-12-01The Munters CorporationReactor column
FR2518713A1 (en)*1981-12-211983-06-24Moreau ChristianEvaporative air freshener for vehicle - has housing with moistened surface formed by zigzag absorbent air permeable cloths
US4499031A (en)*1982-09-271985-02-12Allis-Chalmers Corp.Evaporative gas treating system
US4544513A (en)*1983-04-151985-10-01Arvin Industries, Inc.Combination direct and indirect evaporative media
WO1985000021A1 (en)*1983-06-161985-01-03Board Of Control Of Michigan Technological UniversColumn froth flotation
US4592834A (en)*1983-06-161986-06-03Board Of Control Of Michigan Technological UniversityColumn froth flotation
US4599174A (en)*1984-02-271986-07-08Polybac CorporationSubmerged fixed film biological treatment system
US4842778A (en)*1985-12-231989-06-27Glitsch, Inc.Apparatus for flow distribution in packed towers
US4678615A (en)*1986-07-231987-07-07Dspie "D. Blagoev"Cooling stack for cooling towers
US4950430A (en)*1986-12-011990-08-21Glitsch, Inc.Structured tower packing
US4934663A (en)*1989-09-201990-06-19Phelps Peter MCooling tower with sloping high density film fill sandwiched between low density film fill
JP3273611B2 (en)1992-01-212002-04-08アルファーラヴァル サーマル アーベー Plate heat exchanger
US5192464A (en)*1992-04-231993-03-09Lech PawlowskiEvaporative cooler
US5312464A (en)*1993-05-251994-05-17Munters CorporationCross-flow film fill media with drift eliminator
US5762668A (en)*1996-07-241998-06-09Glitsch, Inc.Apparatus and method for deentrainment in a chemical process tower
US6502807B1 (en)*1998-08-252003-01-07Agam Energy Systems Ltd.Evaporative media unit for cooling tower
WO2000011426A1 (en)*1998-08-252000-03-02Agam Energy Systems Ltd.Evaporative media unit for cooling tower
WO2003004937A1 (en)*2001-07-032003-01-16Agam Energy Systems Ltd.An air conditioning system
US20030086846A1 (en)*2001-11-052003-05-08Adusei George Y.Monolith stacking configuration for improved flooding
RU2262455C1 (en)*2004-06-302005-10-20Московский автомобильно-дорожный институт (Государственный технический университет)Air cleaner
US20080116592A1 (en)*2005-01-112008-05-22Ff Seeley Nominees Pty LtdMethod and Materials for Improving Evaporative Heat Exchangers
US8636269B2 (en)2005-01-112014-01-28Ff Seeley Nominees Pty LtdMethod and materials for improving evaporative heat exchangers
EP1836046A4 (en)*2005-01-112013-12-11Seeley F F Nominees METHOD AND MATERIALS FOR ENHANCING EVAPORATION HEAT EXCHANGERS
US20110220333A1 (en)*2005-01-112011-09-15Ff Seeley Nominees Pty LtdMethod and materials for improving evaporative heat exchangers
ES2326851A1 (en)*2005-05-052009-10-20F F Seeley Nominees Pty LtdAn evaporative material system and method of manufacture
US20060292349A1 (en)*2005-05-052006-12-28Seeley Frederic FAn evaporative material system and method of manufacture
ES2326851B1 (en)*2005-05-052010-07-15F F Seeley Nominees Pty Ltd METHOD OF MANUFACTURE OF EVAPORATIVE MATERIAL.
US20070145611A1 (en)*2005-12-232007-06-28Lee Adam TGas-liquid contactor baffle
US7445200B2 (en)2005-12-232008-11-04Amt International, Inc.Gas-liquid contactor baffle
US7648128B2 (en)2006-12-222010-01-19Amt International, Inc.Gas-liquid contact apparatus
US20080150171A1 (en)*2006-12-222008-06-26Amt International, Inc.Gas-liquid contact apparatus
US7753348B2 (en)2007-01-302010-07-13Amt International, Inc.Gas-liquid contact apparatus
US20080179766A1 (en)*2007-01-302008-07-31Lee Adam TGas-liquid contact apparatus
US20090189301A1 (en)*2008-01-242009-07-30Amt International, Inc.Downcomer distributor
US8070142B2 (en)2008-01-242011-12-06Amt International, Inc.Downcomer distributor
WO2010089315A3 (en)*2009-02-042013-04-25Universität KasselSystem for dehumidifying, heating and/cooling of a liquid
US9109839B2 (en)2013-06-112015-08-18Akeel Ali WannasMulti-layered evaporative media module for heat exchange apparatus
DE102018120217A1 (en)*2018-08-202020-02-20Tristan Wilms Device and method for the simultaneous biological purification of waste water, in particular waste water with a biodegradable load, and provision of cooled air
WO2020038896A1 (en)2018-08-202020-02-27Tristan WilmsDevice and method for simultaneous biological purification of waste water, in particular waste water laden with biodegradable pollutants, and provision of cooled air
USD1071114S1 (en)*2023-03-242025-04-15Yu-Sung LiHeat dissipation mesh

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Publication numberPublication date
SE318587B (en)1969-12-15
DE1302032B (en)1969-10-16
DE1302032C2 (en)1975-12-18
GB1118452A (en)1968-07-03

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